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The feasibility of manufacturing narrow polydispersity polymers in continuous flow systems is explored. The method of moments is applied to ideal and more realistic kinetic schemes in a variety of reactor types. In most cases, polydispersities approaching those obtained in batch can also be achieved in continuous reactors, but the long-term stability of a tubular reactor with species-dependent, radial diffusion remains in doubt.
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Kim et al. (1997) studied this question.
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